Process and apparatus for utilizing zeolites



Oct. 4, 1927. 1,644,469

w. H. GREEN v PRocEss AND APPARATUS FOR UTILIZING ZEOLITES Fild June a, 1923 2 Sheets-Sheet 1 Oct; 4 192 7 w. H. GREEN PROCESS AND APPARATUS FOR UTILIZING ZEOLITES 2 Sheets-Sheet 2 Filed June 8, 192-3 Patented Oct. 4,1 927.

UNITED STATES PATENT OFFICE.

WALTEEH. GREEN, or oHIoAoo, ILLmoIs, ASSIGNOR, BY MESNE nssreumnn'rm m GENERAL IZEOLITE COMPANY, or omoaeo, ILLINOIS, A oonrona'rron OF ILLINOIS.

rnoonss AND APPARATUS non UTILIZING znonrrns.

Application filed June -8,

This'invention has to 'do with the provision of a process and suitable apparatus for utilizing to the best advantage the base-exchanging properties of zeolites, and has par- '5 ticular reference to practices wherein the required contact between the liquid to be purified and the zeolites is effected by. filtration or percolation. The employment of zeolites has been ad- I vocated for the softening, demanganizing and deferrizing of water, for thepurification of sugar juices and for other purposes, the literature on each subject disclosing the nature ofthe exchange, the composition of the particular zeolites involved and of the regenerating solution required. Having been most extensively employed for removing the constituents which cause hardnessin water, the specification herein will be directed to that particular practice, although the invention may be utilized to advantage in the other fields, as the composition of the zeolites and the character of the regenerating solution will not alter in any material respect the procedure or the apparatus contemplated herein. In the art of softening water by the use of zeolites it has been the customary practice to employ a bed of zeolites in a filter casing, to pass the water to be treated through zeolites containing sodium, upon exhaustion of the zeolites to cut off the flow of hard water and to saturate the zeolites with a regenerating solution of sodium chloride,.then to wash out the brine, after which the softening operation may be resumed. In some cases an intermediate step of back-washing the zeolite bed to remove mechanically separated impurities is involved.

During the time required for reconditioning of the bed which, with certain kinds of commercial zeolites, requires four or more consecutive hours, and with others, shorter but much more frequent periods, the unit is out of operation so far as the delivery of softened water is concerned, wherefore it follows that regeneration of the zeolites must be effected during periods when there is likely to be no immediate demand for softened water. It frequently happens that these periods do not coincide with the necessity for regeneration so that uneconomical operation is the result. As a solution for the difficulties thus encountered large storage tanks for softened water have been advo- 1928. Serial No. 644,085.

ment and involves additional expense and room. In allcases the attendance of an operative is required to manipulate the apparatus for the accomplishment of the reconditioning steps, and on the whole the practice has been rather ha hazard, unscientific and not altogether satis actory.

The primary object of the present inven tion is to provide a process and suitable a paratus for effecting regeneration of t e zeolites at intervals determined by their capacity for further softening action, without interfering with or interrupting the contin ous supply of softened water from the um A further object is to divide the bed into active and subjective portions; to retain in the active. portion only zeolites having capacity for softening and to remove the same as they become exhausted to the remaining portion for subjection to a revivifying exchange with the base of a suitable regener ating solution. 1

A further object of the invention is to provide a process and apparatus for eliminatin unproductive areas in the zeolit'e bed, whic is accomplished by passing each particleof zeoli'te having capacity for softening water through the region of greatest softening exchange activity, and when it becomes exhausted removing it for regenerating treatment, after which it is again placed in the region where its restored powers may be Y utilized.

An additional object of the invention is to economize in investment and operation by carrying on simultaneously within a single casing the softening and delivery of hard water and the regeneration of the exhausted portions of the zeolite bed.

. A still further object of the invention is to provide a method and means for determining the periods when regeneration is required, as well as for setting in operation the instrumentalities whereby such regeneration may be effected. 1

Still further objects and advantages of the invention will become apparent as the same is better understood from alstudy of the desoription of'parts, and explanation of operation, of the preferred form of apparatus a which is illustrated in the accompanying drawings It will be understood, of course, that by illustrating and describing what I now consider to be the preferred embodiment of apparatus suitable for practicing the invention, 1 do not thereby suggest or intend that the invention is limlted in its application, or that the solicited claims are to be narrowed in their interpretation to any details not specifically'referred to therein, for it is reasonably expected that those skilled in the art will be able to take advantage of the principles involved in the disclosure by apparatus and methods of procedure perhaps dissimilar in appearance and arrangement but nevertheless within the scope of the invention as'defined in the, appended claims.

In Fi 1 of the drawings I have shown a schematlc arrangement of the preferred form of ap aratus for carrying out the process involved.

Fig. 2 is a detailed view of the pot and tilting bucket which comprise a substantial art of the timing means for controlling the How of brine and wash water employed for reconditioning and rearranging the zeollte Fig. 3 is ,a plan view of the pot and bucket and shows the mounting and arrangement of the cams for actuating certain of the pilot valves,

Fig. 4 is a longitudinal sectional view through a ilot valve typical of the several herein empl oyed.

Fi 5 1s a sectional view taken through the line of 55 of Fig. 3.-

Fig. 6 is a section through the line 6-6 of Fig. 3.

Fig. 7 isv a section through the line 77 of Flg. 3. v

Fig. 8 is-a sectional view through the line 8-8 of Fig. 3.

Fig. 9 is a longitudinal section showing in detail the construction of a typical hydraulic gate valve such as employed herein.-

Fig. 10 is diagrammatic of the water meter control for initiating the reconditioning steps, and i ig. 11 is a plan v1ew of the water meter arrangements shown in Fig. 10, and

Fig. 12 is a plan view of the pilot valve shown in Fig. 4.

In the drawings The numeral 10 indicates a cylindrical casing provided with a cover 11 and a conical bottom 12. Water to be treated enters the casing through the hard water supply line 13 andthe ports 13", passing through the upper portion of the bed of zeolites 14 and out through the treated water line 15 which leads to the place of use.

A brine tank 16 feeds a regenerating solution for revivifying exhausted zeolites through the brinesupply line 17 which is provided within the casing with ports 17. A pump 18 is connected to the brine line, a check valve 19 being disposed in the line between the pump and casing, it being understood that the present embodiment is designed as'a pressure system. The regenerating solution passes downwardly through the lower portion of the zeolite bed into the zle connected to bell crank lever 26.

Numeral 27 represents a waste pipe into which the nozzle 25 may be directed to carry off the discharge from pipe 23, or the nozzle 25 may .be directed; under the influence of the bell crank lever 26, to discharge against the blades of a Pelton wheel 28.

A pulley 29 on the wheel 28, is connected with pulley 30, on pump 18, by a belt. 31, to operate the pump upon revolution of the Pelton wheel 28. A lead 32 from the hard water supply line 13, empties into the brine tank 16, the flow therethrough being controlled by Wing valve 33 and the float 34.

After the lower portion of the zeolite bed has been reconditioned, and the flow of the brine has been discontinued, in the manner hereinafter to be explained, softened Waterfrom the casing is withdrawn trom the line 15 for repassage through the casing via pipe 35, connection 36', brine supply line 17, pump 18, connection 37 and pipe 38. Pipe 38 terminates in a nozzle 39 which is directed to discharge a jet 40 of softened water up.- wardly into the flared lower end of an open ended, upstanding cylinder 41, which is suspended in the center of the zeolite bed by lOO brackets 42 fastened to the inner wall ofthe casing 10.

The jet creates a current upwardly through the cylinder 41, which carries with it the regenerated zeolite particles adjacent the mouth of the cylinder. A bafile 43, supported above the upper end of the cylinder, by two or more brackets 44, deflects .the current and induces the zeolite particles carried therein to settle back upon the top of the bed, where they are again in the region of softening activity for exposure ito the upward flow of hard water entering through the ports 13.

The steps incident to reconditioning of the The inner face of disk 54 carries a contact point 56, which, upon each revolution of the said disk, engages the contact 57, thus closing the solenoid circuit 58. This energizes the solenoid 59 which is connected to, and, in turn, moves the piston of p1lot valve A.

As in the present embodiment of my 1n vention pilot valves are employedthroughout, in connection with hydraullc gate valves. as the means for controlling such intermittent flows as are involved in the reconditioning of the zeolite bed, a statement of typical construction and operation will suflice, for which reference is made to Figs. 4 and 9.

The pilot valve comprises a substantlally cylindrical casing 61, axially bored to'permit reci rocation of double headed piston 62. The en s of the casing are sealed by screw caps 63. On either side of the transverse center are annular chambers 64-65 in open communication with the piston chamber 66. Water under pressure is received in the piston chamber through. the inlet 67. The piston heads 68 and 69 are so spaced that movement of the piston to the limit in either direction will lace them respectively on corresponding sldes of the openings to chambers 64 and 65. At the rear of the casing 61, openings 79 and 80 from the ends of the piston chamber 66, lead to a waste pipe 71.

A tube 72 leads from chamber 64 (Fig. 4) to the inner end of hydraulic valve cylinder 73 (Fig. 9), a corresponding tube 74 connecting chamber with the outer end of cylinder 73. A piston 75 has its rod 76 connected to a gate valve 77, the latter'con trolling the passage of water through the pipe X. In Fig. 9 the valve 77, is shown to be open, the dotted lines indicating the position of the piston and the valve when the latter is closed. The opening of valve 77 is effected in the following manner:

Movement of the iston 62 to the extreme left, as shown in Fig. 4, opens direct communication between inlet 67 and chamber 64, but cuts off direct communication with the chamber 65. Water under pressure, taken from hard water line 13, enters the piston chamber 66 through inlet 67, passing.

through chamber 64 and tube 72 into ,the inner end of cylinder 73, forcing the iston 75 (Fig. 9) to the right. Piston rod 6 being connected to valve 77 withdraws the valve thus leaving a free passage through the 1pc X.

.ater in the cylinder 73 on the other or outer side 'of piston 75, isforced up through the tube 74, chamber 65, and out through opening 80 to the waste pipe 71. To close gate valve 77 the flow is merel reversed, piston 62 being moved to the rig t, opening a direct communication between inlet 67 and chamber 65, thus causing the water under pressure to pass through tube 74 to the outer endof cylinder 73, moving piston 75 and valve 77 to the position shown in dotted appropriate chamber and tube of valve A to 'open hydraulic gate valve A thus permitting water to'flow from line 13 through pipe. 82.

The frequency with which valve A is opened depends upon the time taken for the disk 54 to make a "complete revolution,

which, in turn, is controlled by the amountof hard water passing through the water meter 48. By raising or lowering the disk 53 on the shaft 49, the speed of revolution of disk 54 can be 'accordmgly increased or diminished, thus enabling a control of the operation of valve A based upon the passage of any predetermined volume of water in the'casing 10. If the water being treated contains more or less than the usual degree of hardness, the opening of valve A may be timed accordingly by variation of the place of contact between disks 53 and 54.

The pipe 82 may empty directly into an open tilting bucket 83, mounted loosely on the shaft 84, by hubs 86 at the bottom of the bucket, or it' may empty into the ot 102 which drains into bucket 83. The s aft 84 is journaled in standards 85 which rest upon a base 87. i The sides of the bucket 83 are triangular 1nshape, with the long le' normally at the front, the short leg at t e. rear, and the hypotenuse at the top. A counterweight 88 adjustablyconnected to the .rear of the bucket, in conjunction with an adjustable support 89, serves to hold the 'bucketin up- 'r1 ht position when empty.

e ed to the shaft 84 in the relation shown in FlgS. 5, 6, 7 and 8, are four cam wheels- 91, 92, 93 and 94, each having a cam groove 9n 1ts face, a portion of which groove is adacent and there concentric with the periphery of the wheel. The outer portion of the groove 1n cam 91 extends over a segment constltuting the first three-quarters of the wheel. In cam 92 the groove extends only over the filst quarter, cam 93 over the second quarter and cam 94 over the third quarter.

A roller 95, traveling in the groove of cam 91, is connected to the piston 62 of pilot valve B.v A roller 96, engaged in the groove of, cm 92, is connected to piston 62 of pilot draulic valve B in the brine discharge pipe 23." Pilot valve C, through tubes 72 and 74,

operates hydraulic valve'C, which is placed in the brine supply line 17 between the tank .16 and'the pump 18, and also operates valves C" in the brine" line between the pump and the casing 10. Pilot valve D, through tubes 72 and 74, operates the piston in cylinder 1), which is connected. to the bell crank lever 26. Pilot valve E, through tubes 72 and 74?,operates the hydraulicvalve E in pipe 35 and the valve E in pipe 38. The pressure supply for these fourpilot valves are respectively inlets 67, 67, 6: and 67 all leading from pipe 13. l

During th flow. of regenerating solution and of wash water, a b -pass 99 leadingfrom a reducing T 101 in t e brine discharge 23, empties into the pot 102, the latter being supported by columns 100 standing upon the base 87. The pot 102 is positioned directly above-the bucket 83, and has an orifice 103 in the bottom thereof into which a'tapered' plug 104 may be raised and lowered. respectively toincrease and decrease the effective size of the orifice. The plug is suspended from a vertically extending rigid arm 105, secured to a horizontal bracket 106, the latter being adjustablyfastened to the vertical reciprocating rod 107 by a collar 108 and set screw 109, the rod being slidably held in slotted arms 110 and 111, and its downward movement being limited byengagement' of the collar 108 with the arm 110. The rod 107 is provided with a horizontal bearing plate 112 at its, lower extremity, the plate projecting into the plane of a lifter wheel 113, which wheel is keyed to the shaft 84 adjacent one side of the tilting bucket '83. The wheel 113 is provided on its inner face with an annular ratchet edge 114, composed of four teeth. A pawl 115, which is secured tothe side of the tilting bucket 83 adjacent the wheel 113, is adapted to en age the ratchet 114, and upon each forwar tipping of the bucket, turns the wheel 113, the shaft 84 and each of the cams 91, 92, 93 and 94, one-quarter of a revolution. On the rim of the wheel 113, four adjustable radially projecting fingers 116, 117, 118 and 119, of different' lengths, are provided. Upon revolu-.

. tion of the wheel these fingers are adapted successively to engage the lower'face of the bearingvplate 112, and correspondingly to raise or lower the rod 107, and thereby the plug 104, to vary accordingly the effective sizeofthe orifice 103. s

Inthe operation of the apparatus which hasbeendescribed, hard water under pressureenters the casing 10 from inlet'pipe 13,.

passing from the ports 13 through the upper portion of zeolite bed 14, leaving as softened water through the outlet pipe 15. After the softening capacity of that portion of the bed adjacentthe inlet ports 13 has been ex: hausted, a regeneration of the exhausted por tion is effected. This is initiated in the following manner: 1

The disk 53 on the water meter indicator shaft- 49 is adjusted with relation to the disk 54, so that the passage of a predetermined volume of water, which will be indicated by the water meter, will cause one completerevolution of the disk 54, bringing into engagement, contact points 56 and 57. This closes the solenoid circuit 58, whereupon the solenoid 59 is energized to move the piston in pilot valve A, which, in turn, opens the valve A in pipe 82. lVater flowing through pipe 82 rapidly fills the bucket 83 which, because of its off-balance construction, tips forward and empties, and in so doing turns the wheel 113 one-quarter of a revolution through engagement of the pawl 115 with ratchet 114. A I

The wheel being keyed to the'shaft 84, correspondingly revolves the latter, carrying through the first one-quarter revolution, each of the cams 91,92, 93 and 94. Incidental to this change in position of the cams,

the rollers 95 and .96 are brought into the outer portions of the grooves of earns 91 and 92, whereby a longitudinal movement is imparted through roller 95 to the piston '62" of pilot valve B, and through roller 96 to the opening of gate valves B C and C in the manner that has already been explained .in consideration of the typical operation of 116. This being the shortest of the :tour

fingers, the plug 104 is consequently in its lowermost operative position, and in cooperation with the orifice 103 permits arelapiston 62 of pilot valve C. This results in v tively slow escape of liquid from the pot 102 into the tilting bucket 83. The flow of brine will continue until such time as the bucket 83 is again filled, when in tipping, the bucket will cause the cam wheels to turn through the second quarter revolution, this retracting the piston 62 of pilot valve C to closegate valves 0 and G and imparting a thrust to the piston 62 in pilot valve D, whichthrust being communicated to the piston in cylinder D rocks the bell crank lever 26 to divert the nozzle 25 from the Pelton wheel to discharge the tapered plug is raised higher, leaving a larger opening throu h orifice 103, in consequence of which the ucket 83 is filled inless time than was the case during regeneration.

The third tilting of -the bucket reverses the piston 62d, thus redirecting the nozzle 25 to discharge against the blades of Pelton wheel 28, and it brings the outer or peripheral portion of the groove in cam wheel 94 into position, where y the piston 62 of pilot valve E is actuated to open hydraulic valves E in pipe 35 and E in' line 38, so that softened water from the pipe 15 will be pumped through the nozzle 39 upwardl into cylinder 41 to rearran e the zeolite be the regenerated portion eing carried to the top of the bed and the exhausted portions dropping to the bottom for subsequent regeneration.

On the. third turn the still longer finger 118 elevates the rod 107 to again increase the eflective size of orifice 103, so that the time now taken to fill the tilting bucket is considerably shortened.

.The fourth emptying of bucket 83 reverses.

the piston 62 in pilot valve B, and .62 in glot valve E, thus closing valves B E and 2 and marking the end of the reconditionin' cycle.

he unit is now".confined to the delivery of softened water,-and will continue so to operate until the quantity of hard water, for Y which the bed is rated, has again passed through the water meter. and brought about the" closing of the solenoid circuit, which initiates a new regeneration.

On the fourth quarter turn ofthe wheel 113, the longest finger 119 is brought into engagement with the plate 112, leaving the effective opening of orifice 103 substantially equal to the diameter of pipe 82, in order that the time of operation incident to the first tilting of the bucket will be the same in case-it is desired to 'dischar e from pipe 82 into the pot 102, rather than 'rectly into the tilting bucket 83.

During the reconditioning of the lower portion of the bed, the flow of hard water through the upper portion for softening, continues uninterruptedly. The capacity of the unit is not dimmished during this period, nor is there any deterioration in the quality of the softened water delivered therefrom.

The bed may be reconditioned as frequently as is desired, and because of the wide latitude in adjustment permissible, the separate steps of the reconditioning may be varied in the time of their duration to fit the require ments of each individual installation. I claim:

1. The process, of softening water which comprises passing hard water continuously upwardly throug a portion of a bed of zeolite, intermittently passing a regenerating sol'ution'downwardly through another portion of the bed, washing out the regenerating solution and then transferring particles of thfi bed from each of said portions to the ot er.

2. The process of utilizing zeolites which comprises disposing a bed of the same in a filter casing, passing a liquid to be purified continuously through a portion of the bed, intermittently passing a regeneratin solution through the other portion of the d then washing the latter portion to remove t e regeneratmg. solution while in the same position and then rearranging the bed to transfer particles from the dormer portion into thelatter portion and from the latter to the former.

3. The process of utilizing zeolites which comprises assin a liquid to be treated continuously t r'oug a portion of a bed of zeolites in one direction, intermittently passing a regenerating solution throu h the remaining portion in a different irection, then washing out the latter portion to remove the regenerating solution and then transferring particles from each portion to the other.

4. The process of utilizing zeolites which comprises assin a liquid to be treatedcon- .tmuously t roug a portion of a bed of zeohtes in one direction, intermittently passing a regenerating solution through the remainated'pa'rticles from the latter portion and.

vice versa.

5. The process of utilizing zeolites which comprises passing a predetermined quantit of liquid to be treated continuously throug 'a portion of a bed of zeolites, intermittently.

passing a regenerating solution through the remaining portion ofthe bed, then washing out the regenerating solution and then after each ntermittent regeneration and subsequent washing transferring regenerated zeolites from the latter to the former portion of-the bed.

6. The process ofutilizing zeolites which comprises passing a predetermined quantity of liquid to be treated through a portion of a bed of zeolites, then passing a predetermined quantity of a regenerating solution through the. remaining portion of the bed, then washing out the regenerating solution treated throu h u er part of the ed, means casing, means for passing a liquid to be treated through a' portion of the bed, means operative upon the passage of a predeterminedquantity of said liquid for passing a regenerating solution through the remaining portion of the bed, and means for washing out the regenerating solution.

9. Apparatus for utilizing zeolites comprising a casing, a bed of zeolites within the casing,- ineans for passing a li 'uid to be operative upon t e passage of a predetermined quantity of said liquid for passing a regenerating solution through the remaining portion of the bed, and means for washing out the regenerating solution. a I

10. Apparatus for utilizin zeolites comprising a casing, a bed ofzeo ites within the casingfmeans for passing a liquid to -be treated through a portion of the bed, means for concurrently passing a regenerating solution through another portion, timing means for starting and stop ing the .flow offregenerating solution for washing out the regenerating cutting of! the supply thereof, and means solution.

- through the prising; a casing;

solution. 1 s i g 11; Apparatus for utilizing 26011138800111- prising a casin a bed of zeolites within the casing, means or passing liquid to be treated through a portion ofthe bed, means for concurrently passin a, regenerating solution through the remaining portion, timing means controlled by the flow of said liquid for starting and stopping-the re enerating flow, and means for washing out. t e regenerating l2. Appliratus for utilizin zeolites comprising a casin a bed of zeo ites within the casing. means or passing liquid to be treated bed, means controlled by the passage of said liquid for concurrently passing a regeneratingsolution tion of the bed, means controlled by" the passage of the regenerating solution for for washing the regeneratingsolution.

13. Apparatus for utilizin 'zeolitescom- I'lv bed of Zoo ites within the casing,- means otpaming a liquid be solution an means effective uponthefstopping of flow of the regenerating through a pfor-' treated upwardly through a portion of the bed, means for passing a regenerating solution downwardly through the remainder of the bed, means for cutting off the supplyof regenerating solution, and means actuated simultaneously with the cutting ofi of the supply of regenerating solution forwashing out the regenerating solution. 14. Apparatus for softening water comprising a casing, a bed of zeolites within the casing, means for passing hard water through the upper portion of the bed, means for passing a regenerating solution through the remaining lower portion of the bed, means for cutting off the supply of regenerating solution and for washing out the lower portion of the bed, and means operative upon completion of the washing for removing zeolite particles from the lower to the upper portion and from the upper to the lower.

15. Apparatus for softening water comprisinga casing, a bedof zeolites within the casing, means for passing hard water through the upper portion of the bed, means controlled by the passage of avpredetermined quantity of hardwater for passing a re-' generating solution through the remaining lower portion of the bed, means for cutting off the supply of regenerating solution and v for washingout the lower portion of the bed, and means for-replacing exhausted zeolite particles in the upper portion of the bed with regenerated particles from the lower portion. I

16. Apparatus v:Eor utilizing zeolites comprising a casing, a bed of zeolites within the casing, means for passing a liquid to .be treated through the upper portion of the *bed, means controlled by the passage of said liquid for passing a regenerating solutionthrou h the lower portion of the bed, means contro led by the passage of the regenerat in solution for cutting off the supply of said solution and for washing out the lower portion of the bed and means for removing zeolite particles from one portion to the other. 1 4

17. Apparatus for utilizin prising a casing, a bed of zeo ites within the casing, means for passing a liquid to be treated through the up er portion of thev bed, means controlled by the passageof said liquid'for passing a regenerating solution through the lower portion of the bed, means controlled by the passage'of the regenerating solution, for cutting off the su ply of said solution and for washing out t e zeolites comlower portion of the bed, and means controlled by the passage of wash-water for I circulatin the zeolite particles from one portion 0 the bed to the other.

18. Apparatus for utilizing zeolites'comprising a casing, a bed of zeolites within the casing, means for passing a liquid to be bucket adapte water for starting through a portion of the bed, the concurrent passage of a regenerating solution, said means comprising a water meter, a solenoid connected to said meter and a valve actuated by said solenoid.

20. Water softening apparatus comprising a casing, a bed of zeolites within the casing, means for passing hard water through the casing, a by-pass, and timing means for regv ulating the flow of regenerating solution through the casing, said timing means comprising a tilting bucket adapted to be-filled from-said by-pass, a cam operated by said bucket, and avalve actuated by said cam.-

21. Water softenin apparatus comprising a casing, a (bed of zediites within the casing, means for passing hard-water through the casing, means for intermittently starting a flow of a regenerating solutionthrough the casing and timing means regulated by said flow for stopping the same, said timing means comprlsing a tilting'bucket, a cam operated by said bucket and a valve actu-' ated by said cam. v

22. Apparatus for softening "water comprising a casing, a bed of zeoliteswithin the casing, means for passing hard water through the zeolites, means for intermittently startin *a flow of a regenerating solution throug said zeolites, a by; as, and

timing means for stopping said ow, said timing means comprising, a tilting.v bucket adapted to be filled from said by-pass, a cam operated by said bucket and a valve actu-. ated by said cam.

23. Apparatus for softening and water, said timin means comprising a tilting to be filled from said, bypass, a plurality of cams operated bysaid bucket and a plurality of va ves actuated by said cams. 1 v

24. Water softenin apparatus comprising means for assing hard water through. the

zeolites, a y-pas', and timing. means for regulating the flow of reconditioning liquids through the zeolites, said timingimeans comprising a tilting bucket, a pot a solution and a jet 0 water comprising a casing, abed of zeolites within the casing, means for passing hard. .Water through the zeolites, means for---.i'ntermittently'startin a flow of a regenerating solution throug said zeolites, abiy pass, and

timing means for stopping sai p cbmprises continuously for starting and stoppingia' flow of wash apted to receive liquids fiom saidby pass andto fin said bucket therewith through an orifice in rality of radial fingers adapted u on revolution imparted by said tting ucket to move't he plug, a cam operated by said bucket and a valve actuated by saidcam,

25. Apparatus forv softening water comprising a closed casing, 'a. bed of zeolites within the casing, means for passing hard water under pressure through said zeolites, and means for intermittently passing a regenerating solution through the casing, said means comprising a supply pipe for said solution, a water meter operated by the passage of the hard water, a solenoidconnected to said meter, a valve ada ted. to be opened by said solenoid, a tilting ucket ada ted to be filled' by a flow of waterthroug v said valve, a camoperated by said bucket, hydraulic valves in said supply line actuated by said cam, a discharge pipeleading from the casing,-.-a wheel adapted to be revolved by the liquid flowing through the discharge pipe and a pump in said supply, line actu ated by said wheel.

ing a. casing, a bed ofzeolites' within the casing, an open ended vertical cylinder dis-' posed in said bed, means for passin hard waterthrough the upper portion of t o bed,

'- means for intermittently, passing a'regenerating solution through the remainder of the bed, means for washing out the regenerating Y soft water directe upwardly in the'lowerendof-said' cylinder for transferring zeolites from the bottom to the top portion offthe bed upon completion of the Washing operation.

27.;Apparatus for utiliz'in zeolites comprising a-casing, a bed of zeo ites within the casing, means for passing throughthe casing a liquid to,be purified by contact with.

the zeolites, means for initiating the concurrent flow ofv a solution through a ortipn of the bedcapable of regenerating t e zeolites, and timing means regulatedby the said flow for stopping the same.

28. The process'of utilizing zeolites which passing a liquid through a portion of a permit' an exchange of bases between the liquid and the zeolites,,intermittently passing through the remainder-of the bed a solutioncapable of regeneratingthe zeolites,

29. Apparatus for utilizing the exchange property of zeolites comprising a casing, a

ed of zeolites to then removing the regenerated zeolites to I "another portion of the bed. a casing, abed of zeo tes wlthm'the casing,

bed of zeolites within the casing, means for x continuously passing aliquid to be altered by 'the exchange through a portion of the bed of zeolites, 'means for passing a solution capable of regenerating the zeolites through the remainder of the bed, and timing means for starting and stopping the "liquid to be passage of the regenerating solution.

30. Apparatus for utilizing the exchange properties of. zeolites comprising a casing, a bed-0f zeolites within the casing, means for continuously, passing through the bed a altered by contact with the zeolites, and ad'ustable means controlled by thevpassa'ge 0 said liquid for intermittently passing through the bed a solution-capable of regenerating the zeolites. I Y

31. Apparat for util'zing the exchange properties of zeolites comprising a casing, a bedof zeoliteswithin the casing,"means for passing continuously through the bed, a liquid subject to alteration by contact with the zeolites, and means controlled by the passage of predetermined quantities of said passages of predetermined quantities of the liquid for intermittently passing through the bed a solution capable of regenerating the zeolites and means forin termittent-ly rearranging the bed.

32. Apparatus properties of zeolites comprising acasing, a bed of zeolites within the casing, means-for passing continuously through the bed a. liquid subject to alteration by contact with the zeolites, means controlled by 'tllie-passage of predetermined quantities of said liquid for intermittently;passing through the bed asolution capable'of regenerating the zeolites, and means fjco' itrolled by the regenerating solution for cutting off the supply ofsaid solution. a i 7 n testimony whereof I have'here'unto subscribed my name. 1 WALTER H. GREEN." v

for utilizing "the exchange 2 

